INTEGRATED UTILIZATION OF SILICON TETRAFLUORIDE AND ZIRCONIUM DIOXIDE
1903
Fig. 5. Kinetics of the process at various temperatures.
( ) Degree of conversion and ( ) time. Temperature ( C):
(1) 700, (2) 800, (3) 900, (4) 1000.
Fig. 6. Plug-flow reactor for utilization of SiF . (1) Col-
4
umn heated to 900 C, (2) desublimator for collecting ZrF ,
4
and (3) reaction front.
The disagreement between the thermodynamic cal-
culations and the actually observed process may be
due to a nonequilibrium state of the system, whereas
the classical thermodynamic approaches are only ap-
plicable to equilibrium processes. In fact, zirconium
tetrafluoride formed at temperatures higher than 900 C
sublimates and leaves the reaction zone (being de-
sublimated on a cold wall reactor), i.e., the reverse
reaction becomes unfeasible and the overall reaction
occurs even at negligibly small equilibrium con-
stants.
CONCLUSIONS
(1) The results obtained in studying the reaction
2ZrO2 + SiF4 = ZrSiO4 + ZrF4 enable several pro-
cesses: (i) utilization of SiF4, (ii) fluorination of ZrO2
without using F2 or HF, and (iii) production of high-
purity ZrSiO4 for manufacture of Bakor-type mate-
rials.
(2) The data obtained make it possible to develop
a technology for utilization of silicon tetrafluoride
and processing of waste ceramic zirconium dioxide.
The results of kinetic experiments at 700, 800, 900,
and 1000 C are shown graphically in Fig. 5. The de-
gree of conversion was calculated from the weight of
zircon formed. The experimental data allow us to sug-
gest two technological processes: (i) utilization of
SiF4 and (ii) that of ZrO2.
REFERENCES
1. Galkin, N.P. and Krutikov, A.B., Tekhnologiya ftora
(Technlogy of Fluorine), Moscow: Atomizdat, 1968.
2. Galkin, N.P., Zaitsev, V.A., and Seregin, M.B., Ulav-
livanie i pererabotka ftorosoderzhashchikh gazov (Re-
covery and Processing of Fluorine-containing Gases),
Moscow: Atomizdat, 1975.
3. Korovin, S.E., Drobot, D.V., and Fedorov, P.I., Redkie
i rasseyannye elementy, khimija i tekhnologija (Rare
and Scattered Elements, Chemistry and Technology),
Moscow: Mosk. Inst. Stali Splavov, 1999, vol. 1.
4. Ryss, I.G., Khimija ftora i ego neorganicheskikh so-
edinenii (Chemistry of Fluorine and its Inorganic Com-
pounds), Moscow: Goskhimizdat, 1956.
5. Powder diffraction file. Alphabetical Index of Inorganic
Compounds 1977. International Centre for Diffraction
Data, 1601 Park Lane, Swarthmore, Pennsylvania
19081, USA.
An integrated utilization of SiF4 and ZrO2 can
also be organized. A schematic of the suggested plug-
flow apparatus for utilization of silicon tetrafluoride is
shown in Fig. 6. The apparatus consists of two parts:
a column 1 with granular zirconium dioxide, heated to
900 C, and a cooled desublimator 2 for collection of
zirconium tetrafluoride. Silicon tetrafluoride fed into
the lower part of the column will react with the excess
amount of zirconium dioxide to give zircon and zir-
conium tetrafluoride.
The completion of the process upon arrival of
the reaction front 3 at the upper part of the column 1
can be judged from the appearance of silicon tetra-
fluoride in the vacuum system.
6. Kireev, V.A., Metody prakticheskikh raschetov v ter-
modinamike khimicheskikh reaktsii (Methods for Prac-
tical Calculations of the Thermodynamics of Chemical
Reactions), Moscow: Khimiya, 1975.
RUSSIAN JOURNAL OF APPLIED CHEMISTRY Vol. 76 No. 12 2003